Process and apparatus for recovering metals from their ores.



J. A. POTTER. SESS AMS PEARAT'S FOR REGQERING METALS FBGM THEIR DRES.

LED AUG. 1s, 1909.

APPLGATON n y Patente@ may 31, M3

5 SHEETS-SHEET 1.

mvENT'oR,

` wlTNEssEs ATTORNEY A. PQTTER.,

PROCESS AED APPARATUS POR REGGVERING METALS FRO THEIR -APLIGATION TILBD AUG. i9, 1909. 1,026,999.

VVITNESSES 5.. A. POTTER. PROCESS AND AYPARATUS lFOR RECOVERNG METALS FROM THEIR GRES.

APPLIGATIOH FILED AUG. 19, 1909. 1,026,999. r Panena May 21, 1912.

. 5 SHEETS-SHEET 3.

N NQ m W ATTORN EY J. A, PGTTBR. PROCESS AND APPARATUS FOR RECGVERNG METALS FROM THEIR DRES.

APPLIGATIQN :FILED AUG. 19, 1909.

1,026,999. Patented May 21,

5 SHEETS-SHEET 4.

, *n "13' maf E" L J. A. POTTER. PROCESS AND APPARATUS POB. REGOVERING METALS FROM THEIR DRES.

APPLICATION FILED `AUG. 19, 1909.

r19911tee'lmay 21, 1912.

f5 SHEETS-SHEET 5.

INVENTOR Mlm 37M ATTOR EY Y Orcs,

UNITED srATEsrAraNr carica.

vJOHN A. POTTER, OF LOS ANGELES, CALIFQRNIA.

PROCESS AND' APPARATUS FOB. REGVERING METLS FRIVS THER GRES.

To all whom 'it may concern:

- Be it known that I, Jox-IN A. Porre@ a citizen of'tne United States, residing at Los Angeles, in the county of Los Angeles and State of California, have .invented new and useful Improvements in Processes' and Ap parat-us for Recovering Metals from r`l`heir of which the following is a specification.

The presentinvention/relates to an iniproved process and apparatus for sinelting,

roast-ing, calcining, and sintering all grades Vof ores,-earths andthe like, the object of -thel invention being to provide a process and apparatus by Whlch the above results will be obtained with heretofore. r

-In the'accompanying drawings, .ligure 1 1s a plan view of my' improved appzuatus;

2 is a longitudinal section-thereof; Fig.

n' 3 is a cross section of the line 3 3 of Fig. 1;

Fig. 4 1s across section of the line '4e-4 ot"A Fig. '1; Fig. 5 is a broken front view of the apparatus; Fig. 6 lis a vertical section showing a .modification ofthe front portion of t-he a. paratus. y Y

Re erring to the'l drawing, 1 indicates columns, and 2 indicates gir-ders supporting Vthe floor 3 of afurna'ce' 4,' said door being formed with two basins 5, for receiving the.

molten metal and slags obtained from the ores. From these basins the molten :metal and slags canpbe drawn intermittently into ladles, as desired, through tap-holes 6, 7. The ore is supplied 4into hoppers 9, located on the top of charging boxes 10, and passes through the bottom of these said boxesfrom which it is, by means of plunger's 11 actuated by 'eccentrics 12, ad-

and desulfurizing'chamber 13, near the bot- .vanced into ldeoizidizing or desulfuriziug chambers 13, located 1n the rear of correspondlng furnace basins 5. The furnace and deoxidizing chambers are provided with suitable doors 14. 4 y e y Opening into the rear of the deoxidizing tom are a series of twyers 15, leading from .a twyer flue 16. Opening into the respective ends ofthe'furnace are larger upper conduits 17, 17 and smaller lower conduits 18, 1 the'latter being just above 'the level to ich the molten slag rises in the furnace basins.

At thesides' of thef apparatus, there arel Specification of Letters Patent,

Application le August 1331,

greater economy than vhoppers into y40', by reason of `all being connected by Wire Serial Eo, 513,505.

provided two vertical. series of three regeuerative dues 2U, 2l, 2.., 20", 21', 22. All of these dues connect at thev front end of the apparatus with the furnace; namely, on one side, the rines 2G.v 2,1, lead to the upper conduit 1T, andthe lowest lue 22 to the lower conduit 13, and similarly for the llues 20", 21', .22", on the other side, the upper lues 20, 20, being controlled at said front end by slide valves 23, 23. .ftthe rear end, the lines 20,21, 22, on one side' ot' the apparatus, connect with a common flue 24, and those 20", 21, 22"', on the other side Witha flue 24', said lines 24, 24 being controlled by slide-valves 25, and discharging into the bottoni of a boiler heating chamber 2G, in which is located an annular water drum 27 connected by Water tubes 2S withv a steam dome 19, so that steam may be generated by the Waste heat from the flues. A stack 29 at the top of the boiler produces thenecessary draft, and carries oli" the Waste gases. The uppermost lues 20 and 20 connect at the front end, by passages 30, 30', with the twyerflue 16, said passages being controlled by slide valves 31, 3l.

At the rear of the furnace there is ,provided a pressure fan 32, adapted to be driven by a pulley fronivany suitable source of'pover. Said pressure fan is connected on its vacuum side by an upright pipe 34, controlled by a valve 42, `With .gas supply flues 35. From said fines the gas is drawn by the fan paddles and discharged under pressure ,into the pressure chamber 36. Tlience it passesby a pipe 37 or 37 and through a valve 3S or 38', into the upper regenerative flue 20er 20', as desired. Gas is also conveyed atI ordinary pressure from the uprightgas-pipe 34 by a gas-pipe 39 or 39', and through valve 40 or 40, and into the lower regenerating Hue, 22 or 22', accordingly as the reversing valve mechanisms are disposed. Sliding doors or valves 41,- 41 open or close 'openings admitting air into the middle regenerating H u'es 21 or Patented May 21, 1912.-

21 accordingly as the `reversing''valves are disposed; ,l

.The slide valves 23, 23225, 25", 31, 31, are opened and shut by being moved 'up and down, together With-the slidingdoors 41, 4l" and the gas valves' 38, 38', and 40,

cables or chains to or: over sheave Wheels on a. main reversing shaft 44 and on counter shafts 45, 46, 47, 48, 49, 50, so that, by pullis caused to rotate in the desired direction,

and the whole reversible valve system ris shifted.

The'valves 23, 31, or 23', 31', at either side of the apparatus, are, by means of the above described mechanism, operated in unison, so that the upper regenerating flue 20 or 20' at that side is either closed to the twyer passage 30, 30' and open to the furnace, in which case the gases of combustion pass from the latter along said flue to the stack,

4or is closed to the furnace and open to the twyers, when fuel gaspasses in the reverse direction to the tWyers.

An air valve 5,3 for admitting air to the .Y

pressure fan 32 may be opened at will by pulling down on a handle on the end of a cord 54 attached to a lever 55, thereby permitting the desired amount of air to pass,

to the fan, which air is therebyr forced into and through the pipes and valves 'to the flues21 or 21, as maybe desired. A pipe 56, controlled by a. valve 57, leads from` the chamber 26 to the fan for the purpose of drawing off neutral gases from the'interior of said chamber. i

The following is the method of using the above apparatus for smelting oXid or carbonate ores, particularly-.iron oXid ores, so that liquid wrought iron or all gradesof steel-,are .produced direct from the iron contained in the ores.

The furnace being first heated to a proper degree for smelting, themixed ores and fluxes are fed into the hopper-s 9, from wherethey pass into the charging boxes 10, and there form the ore charges which are to be smelted. At this time, fuel\gas for pipe 39', through the flyvalve 40' into'the regenerative flue 22, where it is preheated, and finds its way .up through the conduit 18' into the furnace combustion and melting chamber 4, where it meets heated'a-ir comin-g into the same chamber through the conduit 17. lWhile this gas is thus passing into the furnace as above described, air is being admitted into the regenerating flue 21 through sliding door valve opening 41, which finds its way after beingheated into the furnace combustion. chamber through the conduit 17', where it meets the gas flowing'through the'eonduit 18', .as above eX- plained. New, while the fuel gas and air .are being conveyed to the combustion chamber, as described above, reducing gas and discharged into pressure chamber 36 afhence it is forced into branch pipe- 37', and through. the valve 38' into the regenerating flue 20', Where it is highly heated while on its way forward, Where it finally encounters the valve 23 which is now 70 closed, and finds its way 'into the-tvvyerV passage 30, passing under the Valve 31',` which is now open, then accumulating in4 the flue 1G, whence it is unable to escape, as the valve 81 at the other end is, closed, so that the heated gas is compelled to vpass n into and through tWyers 15, into an through the ore charges. Now, this gas has beenpreheated to a very high` degree, say, about 2500O F. and it forms a most perfect medium to preheat the ore charge while passing into and through it. At the same time, since this gas is composed of reducing elements, as hydrogen and carbon, in vary-- ing proportions according to its source of supply or manufacture, t-he hydrogen and carbon contained in the' gasa'ttract, attack and combine with the oxygen contained in the heated ore charges, thusproducing great heat, and changing the oXids of the ore charges into metallic masses of a spongy,

`honey-combed character, which are quickly melted into a liquid state by the high heat,

about 3500o F., maintained in the melting and combusting chamber 4 of the furnace, Which'heat is produced, rst, by the combination ofthe reducing gas and oxygen in the ores, second, by that of the fuel gas and air coming into said chamber through the ports 18' and 17', and, third, by the complete -combustion of the heated carbon Inonoxid gas escaping through the fusing, slagging, and deoXidizing ore charges in numerous gas jets, which discharge into the furnace .chamber and there come in contact with the excess of heated air-'that is coming into the chamber through the port 17 lVhile this deoxidizing, fusing and melting action is proceeding, the feeding mechanism i.

12 is constantly pushing forward fresh ore 1'10 charges, and the fusing and liquid metals Iand slags are constantly flowing down from the fusing o re charges, and finally pass into4 the'furnace basins 5, where'they find their respective levels, according to their specific 11?, gravity, and whence they are intermittently withdawn, as desired, through the tapholes G and 7, linto ladles, by which they may be disposed of as further manufacturing may require. 'During this time the -120 waste gases are passing from the furnace by the flues 20, 2l, 22, to the boiler and stack, thereby highly heating the checker work in said `flues.

After a time, necessary to'stop the flow of the ingoing gases and air through the lues 20', 21', 22 and'to cause them to pass through the flues 20, 21, 22, and at the same time to reverse the direct-ion of vthe out-flow`1ng gases of com- 13G say, 'one hour, it becomes 125:,

and closing the air sliding door 41', thus boiler stack, and in this manner new heats l now coming into the same chamber from the bustion. This reversal is accomplished by the furnace attendant pulling down on the hand chain 51 that passes over the large. sheave Wheel 52, -thereby causing the main reversing shaft 44 to rotate, which raises the valves 23, 25 and 31, while at' the-same time loweringvalves 23, 25, 31', also opening the gas fly valvesV 372i and 40, and closing the gas fly valves 38" and 40, and at the same time opening'the air vsliding door Lil causing a complete reversal of ports, tlues, pipes, andV valves, for the gases and air flowing to the combustion chamber 4, and the eombus'ted heated gases tlowing to the vgas flues 35 and pipe 134, through the gas Hy valve 42,.which regulates the Vamount of' gas to be mixed with the neutral gas to suit the requirements. Y.

The. above description ofo erationfis iii-- tended to apply to the metho when reducing all classes of oxid and carbonate ores, both 'the Avery refractory ores as oxid of chromium, manganese, iron, nickel, ccpgjier,

andthe like, that requirehigh and medium reducing heat to successfully smelt them; and such ores as contain the precious metals, gold, silver,- copper, lead, zinc, and the like,- or such ores and compounds of metals asre-v quire. less heat, but require gaseous fuel of a strong reducing character to consume the oxygen and gases contained in the ores and to protect the newly formed metals from oxidation, until they find their proper. places in the basin 5. By regulating the heat of the furnace and gases, ores such as the above can be successfully treated Aand the resulting metals preserve .When smelting ores containing excess'sulfur togetherV with metal compounds, and wherea copper, iron and sulfur matte is formed while the earths and fluxes form .slags, the mode of 'operation is the same as ,described above :when smelting l iron ore, with. the following difference. Instead of forcing reducing gas into 'regenerating andt-Wy'er lues, 'and into the ore charges, the attendantwcloses the gas fly valve 42, and

neutral gas .valve 57 then opens the ail?` valve 53, thus permitting air to be drawnby vacuum into the vacuum chamberv of the pressure fan f'whence it 1s drawn, compressed, and driven into the flue? 20, therepre-heated, and passed into twyer Hue 16, and twyers 15, into and through the ore charges 13, where it imparts its heat and oxygen to the ore-charge and excess sulfur. Then, by such combination, still greater heat is produced, above that contained in the heated air, which causes very rapid desulfur-ization and melting of the ore charge into matte and slag, that run down over the face of the fusing ore, and take their respective places in the basin 5, from where they are withdrawn at intervals through the tap holes 6 and 7, as desired. .lVhen pre-` heated air is being forced into and through the ore charges, its volume and heat are regulated to suit the requirements, thereby controlling the temperature of the regenerating flues and the amount of sulfur consumed.

1When Working' very finely divided ores,

as concentrates, and Ithe like, the heated twyer air or gas is prevented from carrying out of the ore charges the tine ore particles' or dust by reason of the scfnpasty crust or coating of 'melting mattes, metals, slags, and the like, that are always forming and always present when smelting, and which cover the'. complete front faces of the ore charges, close all cracks and holes therein, and arrestall ore dust and prevent it escaping from the charge into the furnace chamber. Hence a great advantage is gained by this processwhen smelting all grades of ores, as all ores Contain fines. before, and make them in, charging andheating, that causemuch annoyance with the present smelting devices.

There are times when ores are to be smelt- .edrthat do not contain more sulfur .than is,-

required to form aproper sulfur, iron, copper and precious .metal matte, and it-ls not' desirable tosmelt them in the presence of oxidizing agents orinfluence. In such cases, the air valve 53 is closed, andthe `neutral gas valve 57'is opened, thus permitting-the fan'to draw neutral gas from the boiler heating chamber 26'dischargin`g the same into the upper regenerating flue, as 20, and finally into the .twyers 15 and ore charges, where they impart their mechanical heat to .the ore charges', thus greatly increasing the smelt-ing capacity of the furnace, and at the same time not `oxidizing any of the"sulfur contents of .the-ore charges. At. the same time, they join with the heated gases formed by the combustion of the fuelgas and preheated air coming in. at ports 17l and 18, whereby a. large yvolume. of Waste .heated gases is formed, keeping up the required heat inthe regenerating flues,

. From the above explanation it will be un' derstocdfthat all gradesof ores can be treated successfully by this process as conditions .carry on the operations, to whatever extent4 and heat degrees can be fully controlled particularly as regards gas combination, as ity is possible to'obtain any characterof reducing, oxidizing and neutral gases required, by

' regulating the valve and fanarrangements.

-Of' the three regenerating lues on each side of the,furnace, the two employed for the regular furnace heating have been suc'- cessfully employed for thirty years or more in regular regenerating steel melting furnaces and are not new, and I make no claim for them, but the third regenerating flue I claim is new, that is, the flue 20 or 2 0', forv highly heating.4 under pressure, reducing, oxidizing and neutral gases which are trapped and'conveyed under pressure into twyers 'and n o re charges under the labove favorable conditions, so that the gases or air, after passing through the ore charges,

still contain some combustible material,

which is then combusted by the unburned oxygen orhydrcgen contained in the heated lair or gas' coming in through the ports 17 or 17', or 18 or 18. Also, when smelting ores 'that contain excess sulfur over that required to form a propermatte, then, in

such cases, the excess sulfur is utilized to furnish part or all o-f the heat required to the excess sulfur exists. In suoli cases, less or 'no fuel' gas is used to heat the furnace chamber and regenerating flues. This excess sulfur is consumedby the heated oxygen contained in the air while .passing through the ore charges, in greateror lessA volume. There are also cases when it becomes necessary to mix with the ore charges solidred-ucing materials as finely divided, slack coal, coke, asphalt-um, sawdust, peat, dry vegetable products, or anysolid dry hydrocarbonaceous materials, and in' such cases they are mixed .with the ore charges whilethe olie and fluxes are being crushed and mixed. Ithiay be here noted that in this Vprocess and with this apparatus the orecharge should be crushed, and in no case should they be composed vof materials larger than 'aboutthe size of hickory nuts, While there are no limits as'to the minimum size of the particles, so that the charge may contain flue dust and the like. Hence the process' and apparatus are particularly adapted to smelt fine concentrates, and the like.

When smelting charges jin which are mixed solidreducing agents, above outlined, air,A reducing, orneutral gas can be used alone, or air, reducing, or neutral gases can he, mixed and forced by the fan into and through the regenerator flue 20 or 20, as the case may be, into and through thetwyers and ore charges, thus causing the solid reducing agents to burn and gasifyand co'mbine with the oxygen in the ores, thus gen'- eratingheatand forming gases that, inturn,

` are completely consumed, as previously explained.

Vhen snielting ores containing sulfur,

carbo-nic acid gas and oxygen in varyingH amounts', as ores containing precious and other metals as gold, silver, copper, lead, zinc', etc., weakbr strong, reducing gas is then employed to pre-heat the ore charges and to consume the oxygen and carbonio acid gas'and preserve the sulfur contents of the ore for matte forming purposes and to protect the metals and matte while forming. In such a case little or no fuel' gas need be admitted into the furnace chamber et through the port hole 18 or 1S', as the case may be, but, in its stead, the reducing gas, 'as carbon 'monoxid, thus forming and issuing through and from the hot faces of the ore charges, meets and combusts the heated air then coming in the furnace chamber through the port 17 or 17; hence sutlicient heat is obtained to carry on the process.

A very important feature of thisy process consists of the heat reactions that take place more or less when smelting oxid ores during the dcoxidizingl periods., When oxids of metals are heated toa temperature -of about 25000 F., but never hot enough to melt the oxids, and at the same time reducing gas, heated to about the same temperature as the ore, is brought in contact With the -heated ores under pressure, a great heat is produced, which is caused by the oxygen contained inthe heated ores comhusting with the heated hydrocarbons contained in the reducing gas. But to produce this action successfully and completely, the operations should 'be carefully conducted in the following manner. After the furnace and checker work have beenheated to the vproper temperatures for smelting and the ore charges andthe uxes are in place in the chambers 13, air is admitted through the fan 32 and conveyed through the variousA pipes and valves into and through the generative iiue 20 Wherev it is pre-heated to about 27000 F. and the twyer flue 16, 'and finally through twyersy15 and the ore charge, thereby roasting and oxidizingany impurities contained in the ore charges, as sulfur, arsenic, and the like, and at the samev time heating up the ore charge to atemperature of about 250.00 F. but not to a melting heat. lWhen the ore charge has been thoroughly heated to 25000 F. by the heated airpassing through it, it really has lost little of its oxygen, owing to the fact that the air passing through it, -vvhilel roasting and heating, suppliesl any tlils point vthe furnace is reversed, thus causing the fuel gas and air to discontinue passing through the'ports 18 and 17, and to flow into t e furnace Y chamber through the h iguy heated ailes 21". and 22', whim n this, time the an' valve 53 on top of the fan 32 is forced through the discharge pipe-andA valve arrangements into the regenerator flue 20', Where it is highly heated to about 270()o F., finally' assingV into the twyer flue i6 and throug the twyers 15, entering .and passing intovandthrough the roasted, heated and oxidized ore charge, Where the thermic 4action immediately begins to take place, particularly at Vthe hottest part of the orel charge, whlchfison'the inner f ace'of the ore charge, nearest the combustion chamber.

' The heat thus suddenly produced may reach a temperature of 4000o F1, and the results are asA follows :v The heated reducing gas contains hydrogen ,and carbon, which attack and combust with the oxygen con# tained in. the ores, causing great heat, that melts andfrees the metal, while at the same time slagsare formed by the association of the fluxes and earthy mat-ters, which slag and metal flow 'down over faces of the ore charge, finding their respective levels according to thelr specific gravity in furnace basin 5, land thus a roasting and smelting plrocess 1s accomplished lnone operation and I rnace. Oxi'd ores vary much in their `refractory character, hence varying heats are necessary to suit the ore tr ated. rI he above description is for refractory ore. In Working the apparatus and process 1n th1s manner the process is not continuous, as one side of the furnace flues are employed to heat ail" and gas, namely', `flue 20 nowheating air to roast and oxidize, flue 21 heating lair for fuel purposes, and flue 22 heating fuel gas.

Then the furnace'reversing mechanisms are operated, and the air vvalve 53 is closed and the gas fly valve 42 isopened, causing reducinggas to flow throughthe iue 20?, fuel air through the flue 21',- and what fuel as is required, if -any,vto flow through the ue 22. About two-thirds of the ore charges will be melted while deoxidizing.` Vhile,

fuel gas willbe needed and used when oxidizing and roast-ing, asy above described, it will not always be used when deoxidizing, as

sufficient heat may be obtained. bythe-chemii cal combination to carry on the process over that period, at'which time the fuel air flowing through the flue 21 will furnish they heated air for completecombustion for any unburned gases coming through the face of ore char e until the'chemicalcombination ceases; w ereuponthe furnace valve mecha nism is reversed back to its .first position, and then oxidizing and roastmg are again carried onvwith the fresh ores charged.

lWhen roasting, calcining, or sintering;

ores, mat-tes, earths, .and the like, a furnace bottom ofa modie'dform i's used, as shown Fig. 6. this modification, the-treated hot material treated as above described -is permitted to tloiv or slide down over the surfacegofjtheunderlying part, as shown at 60,-fro'1fhrthe :roasting and heating chambers 13 and t'following through a hole 61 in the bottom of the furnace chamber, into adis charging trough 62 whence it is conveyed forward by a Worm G3 to'and over anopening 64,-, in the bottom of the trough, whence it drops into a dump car 65, that linally disposes of the materials as desired.

lVhen roasting ores or earths to drive olf the impurities, as sulfur, arsenic and other oxidizable matters, air is introduced into the fan 32 andI forced by itinto pipes,val ves, tlues 20, or 20 and tWyers 15 as above explained, into and through' the roasting materials at such temperatures as are necessary to oxdize and burn out the impurities, but not hot enough to melt the charge, While at the same time the furnace heat is adjusted to suit the occasion by adjusting and controlling the amount of fuel gas and air passing into the furnace .through the regen` erator flues 2l or 21', and22 or 22 and ports 17 or 17 and 18 or 18', and thus this process is economically accomplished on a `large scale.- v

Th-en burning limestone, dolomite, magnesite, marl, and the like, materials which contain carbonio acid or other non-oxidizable gases, air is not used in the raw state for pre-heating, and so forth, but is diluted with reducing gas to any desired extent: or gas alone may be used, or reducing and neutral gases'may be mixed to bring about a proper reducing gas and other conditions to suit the requirements. a

Then calciningjearth and ores as above described, the furnace `heats are controlled to suit the purpose, as previously described, particularlyv When gas, eitherI mixed, or

alone, is used. In such cases the gas, after v passing through the ore charge, issues from the roasting `face ofthe materials and is lthen burned by combusti-ing with the heated air coming into the v'furnace' chamber, through theport 17 or `17 as the case may be.

When sintering materials (generally finely divided materials)l for various purposes, the

furnace heats are raised to a higher degree thanthat necessary for roasting for calclning, as explained above, so as to causethe- 'corners and proyecting parts of the heated materials to` fuse thereby causing `them to :adhere to each other, as they emerge on the exposed, hottest and inner face ofthe sin.- tering material, thus causing the formation -of sintering materials of various sizes, the

inet-hed being particularly adapted-to sinter 'ing finely divided ores, earths, and the like. AThis treatment also deoxidizes and drives o f the impurities from the clinkered ores,

las sulfur, arsenic, and other i1npurities,

lthis being effected by the heated oxygen contained in the air employed, thus being a very valuable result of t-he operation.

In some cases of roasting, calcining and sinteringreducing gases, either lean or rich, may be introduced through `the charge instead of air, thus bringing about a partial reduction of their oxygen or carbonio acidv gases as may be desired by, first, forcing heated air through the charge to 'burn and oxidize its oxidizable contents, and then, by shifting and reversing the valves 42 land gas is causedvto take the place of air, so that a reducing gas is no7 passed through the heated oxidized charge, and, combines With the oxygen thereof, While the gases, weaker in oxygen, as monoxid, issue from the charge face intothe combustion chamber, Where they are burned, and thus assist in maintaining the heat necessary to carry on the process. This procedure is very desirable when burning limestone containing sul'- fur, and the like, also when calcining and sintering'ores, earths, and the like. Also vWhen sintering finely divided precious metal ores, or the like, gas may be used alone so as tov prevent the oxidization of metals contained; also neutralgas can beused toA sin-v ter ores and preserve the met-als.

Itis to be understood that, in my inven' tion, I contemplate the employment of a furnace containing one or Amore deoxidizing or desulfurizingchambers under the same roof.

I claim l. In an apparatus of the character described, the combination of a furnace, a deoxidiZing-chamber opening into said furnace, a stack, tivo' series of regenerative flues arranged to conduct Waste gases from the furnace to the stack, a conduit'leading from4 a4 flue` of eachseries to said deoxidizing chamber to conduct gas thereto, a conduit for supplying combustible gas, an air suply conduit, and vvalves for each series,

adapted to be arranged, in one position to permit the Waste gases to pass through said flues from the furnace to the stack and in another'position to permit airandcombustible gas to pass from said -supply conduits to the furnace and deoxidizing chamber,

substantially as described.

-2. In an apparatus of-the character described, the combination of a furnace, a de oxidizing chamberzopeninginto said furnace. a twyer chamber adjacent, to said deoxidizing chamber and having tWyers lead* ing therefrom into said deoxidizing chamber, means for charging ore iito said deoxidizing chamber, a stack, two series of regenerative fines arranged to conduct Waste gases from the furnace to the stack, a conduit leading from va flue of each series to said tvvyer chamber to conductgas thereto, a conduit for supplying combustible gas',

an air supply conduit, and valves for eachv series, adapted to be arranged in one posi'- tion to permit the Waste gases to pass through said iiues fromthe furnace to the stack and in another position to permit air and combustible gas to pass from said supply conduits to the furnace and twyer chamber, substantially as described.

3. In an apparatus of the character described, the combination of a furnace, a deoxidizing chamber opening into said furnace, a twyer`cha'mber adjacent said deoxidizing chamber and having twyers leading therefrom into-said deoxidizing chamber, means for licharging ore into said de oxidizing cha er, a stack, two series of regenerative fluls gases from the furnace to the stack, a conduit leading from a flue of each series to arranged to conduct Waste said twyer chamber to conduct .gas thereto,

a conduit for supplying combustible gas, an air supply conduit, and valyes for each series, adapted to be arranged in one position to permit the Waste gases to pass through said flues from the furnace to thei stack and -in another position to permit combustible gas to pass to the deoxidizing chamber and combustible gas and air to Apass to the furnace, substantially as described.'

4. 'In 'an apparatus 'of the character described, thel combination of a furnace, a de- 'oxidizing chamber opening into said furnace, a twyer chamber adjacent said de-f oxidizing chamber and having tWyers leading therefrom into said deoxidizing chamber, means for charging ore into said deoxidizing chamber, a stack, two series of regenerative tlues arranged' to conduct Waste gases 'from the furnace to the stack, a conduit leading from a flue of each series to said tWyer chamber to'conduct gas thereto, a conduitfor supplying combustible gas, an air supply'conduit, valves for each series, adapted to be arranged in one position to permit thewaste gases to pass through said vfiues from the furnace to the stack and in another position to permit air and combustible gas to pass from saidsupply conduits to vthe furnace and deoxidizing chamber, and a fan for forcing air andcombustible gas along flues to said furnace, substantially as described. f

5. In an apparatus of the character described, the combinationy of a furnace, a deoxidizing chamber opening into said furnace, a twyer chamber adjacent said deoxidizing chamber and having twyersv leading therefronrinto said deoxidizing chamber, means for charging ore into, said deoxidizing chamber, a stack, two series of regenerative flues arranged to conduct Waste vgases from the furnace to the stack, a con- Loader adapted to be' arranged in one position to permit the Waste gases to pass through said flues from the furnace to the stack and 1n l another position to permit. combustible gas l to pass to the deoxidizing chamber and conibustible gas and air to pass to the furnaceTr and a fan for forcing combustible gas 'to said deoxidizing chamber and air to said furnace, 'substantially as described.

6. In an apparatus of the character described, the combination of a furnace, a dev oxidizing chamber opening into said nace, means for charging ore into said oxidizing chamber, a stack, two series of regenerative flues arranged to conduct Waste gases` from the furnace to the stack, a conduit leading from a flue of each series to said deoxidizing chamber to conduct gas thereto, a conduit for supplying combustible gas, an. air supply conduit, Valves for cach series, adapted .to be arranged in one position to permit the Waste gases to pass through said iiues from the furnace tothe stach and in another position to permit air and combustible gas to pass from said supply conduits to the furnace and deoxidizing chamber, a, conduit leading from said stack to said Hues, and a ,valve in said conduit permitting neutral gases to pass from the stack to the' fines with the combustible gas and air, substantially as described.

7. In an apparatus of the character described, the combination of a furnace, a deoxidizing chamber' opening into said furnace, means for charging ore into said deoxidizing chamber, a stack, tivo series of regenerative fines arranged to conduct Waste gases from' the furnace to the stack, a conduit leading from a `flue of each series to said deoxidizing chamber to conduct gas thereto, conduit for supplying combustible gas, an air supply conduit, valves for each series, adapted-to be arranged in one position to permit the 'Waste gases to pass through said flues from the furnace to the stack and in another position to permit air and combustible gas 'to pass from said Asunply conduits to the furnace and deoxidizing cha nber, a fan for .forcing air and com e gas along lines to said furnace, and a co uit ieading from said stackto 'the in- 1 -r c of fan, substantially dehpparatus of ci ""ter dethe com auatic; a further, a deo. chamber open ing 'into saidA fue nace, means for charging eore into said de; voxidizing chamber, a stack, two series of regenerative flues Waste gases from the furnace to the stach, a condult leading from a-ue of each series ocscribed arranged to. conductsaid deoxidizing chamber to conduct gas etc, a conduit forv supplying combustible an air supply conduit, valves for each adapted to be arranged in cneposi- -cn to permit the WasteA gases to pass ,i said iiues from the furnace to the `ind in another position to permit air an( combustible gas to pass from said supply. conduits to the'furnace and deoxidizing chamber, and means for opening the val4 es cn one side of the iiues and closing thos'e on the otl er, and conversely, substantially as described. i

3. The process of treating ores pfliici'i consists in passing waste gases from a furinace to a stack through a series of lues to highly heat the saine, then closing the passage through sa' l fines to the stack to prei' vent passage of said Waste gases, and passi ing in the reverse direction, through one of said fines fuel 'to the lower part of said furnace, through another of said flues air into the upper part of said furnace, and through the third of said flues reducing gas, discharging said gas into a reducing cha1nber, continuously feeding ore into said reducing Chamb@ in front 'of the discharge opening of said reducing gas, and applying the he; t of combustion ofthe fuel gas in said furnace to assist said reducing gas in neit-ing the ores in said reducing chamber, then conducting the Waste gases so derived -thrruigh a similiar series of regenerative .mentioned fines, substantiallyr as described.

10. rihe process of reducing ore which consists in utilizing the Waste gases ofthe furnace to heat three regenerative flues, then preventing the escape of waste gases through said tlues, and passing in the reverse direction, through tivo of saidy flues respectively, fuel and compressedair, and maintainl ing the said gas and air separate until they meet and combine in the furnace,'continuously charging ore into a furnace in such a diectic-n that the front face of the charge 1s exposed to the .fiames of combustion of Vaid fuel gas by said air,passing through the third iiue reducing gas under pressure, and passing the gas thus highly heated into and. through said charge, substantially as` ln testimony whereof, I have hereunto set my liano 1n the presence of .two 'subscribing Witnesses.

litnesses .Y

Luo/Y E. WHEELER, H. LHcssnY.

.T01-IN A. POTTER. fi'. 

